Successful Solution for High Nitrogen Content Wastewater Treatment from Rendering Plants
Abstract Specific composition of wastewater from rendering plants requires sophisticated approach to treatment. COD content up to 10 g/l and nitrogen up to 2,5 g/l leads to many difficulties during treatment with activated sludge process. Performance of such wastewater treatment plants is generally very unstable: severe problems with filamentous and viscous sludge bulking occur due to macronutrient deficiency, nitrification is often inhibited by high ammonia and nitrite content, no sufficient carbon source for denitrification is available, high temperatures up to 40 °C negatively influence treatment processes. Appropriate control of pH, temperature, biocatalytic nutrient dosage, suitable external carbon source and restriction of inhibitory effects led to successful operation of 4 wastewater treatment plants in the region reaching required effluent standards TIN = 60 mg/l and COD = 200 mg/l.
Keywords Activated sludge, high nitrogen pollution, nitrification inhibition, rendering plant, sludge bulking
Successful Solution for High Nitrogen Content Wastewater Treatment from Rendering Plants
P. Auterská*, L. Novák**
*ODOUR, s.r.o., Dr. Janskeho 953, CZ 252 28 Cernosice,
**AQUA-CONTACT Praha, v.o.s., Buzulucká 6, CZ-16000 Prague 6, Czech Republic, libor.novak@aqua-contact.cz
Introduction
Over the
Technological process for animal material destruction is similar for all these factories. It consists of thermal animal material destruction under minimum temperature of 133 °C and pressure over 3 MPa with duration of 20 minutes as a minimum. During sterilization period the temperature and pressure must be maintained, followed by a period of lower pressure and temperature of about 100 °C. By lowering the pressure, approximately 5 % of water is evaporated. During drying process another 60 % of water is evaporated from the material. Final product contains between 1 to 3 % of water. Condensate from the evaporation is highly polluted wastewater with extremely high content of organic compounds and nitrogen.
In spite of the fact, that some special technologies for treatment of such wastewaters are available at the market at present, in the
Plants description
Since 2003, four WWTP with unsatisfactory operational performance were monitored, sampled, technologically analysed and step by step controlled with respect to improve their effluent parameters. The first three plants are situated in the
Table 1. Characteristics of influent wastewaters and required effluent standards.
|
Item |
Unit |
ASAVET Birkov |
ASAP Vez |
AGRIS Medlov |
Kafiléria SENEC |
Effluent standard |
|
Q |
m3/d |
278 |
260 |
253 |
230 |
- |
|
BOD5 |
mg/l |
3206 |
6300 |
3953 |
5459 |
30 |
|
COD |
mg/l |
4333 |
9000 |
5351 |
6999 |
200 |
|
TSS |
mg/l |
393 |
1100 |
533 |
2720 |
30 |
|
TN |
mg/l |
1022 |
1523 |
1254 |
777 |
60* |
|
COD/TN |
- |
4,2 |
5,9 |
4,3 |
9,0 |
- |
* as TIN for CZ, as TN for SK
Table 2. Technological characteristics of wastewater treatment plants.
|
Item |
Unit |
ASAVET Birkov |
ASAP Vez |
AGRIS Medlov |
Kafileria SENEC |
|
|
System scheme |
- |
R-D1-N1 -D2-N2 |
D1-N1- D2-N2 |
Ist stage D1-N1 |
IInd stage D2-N2 |
R-D-N |
|
Reactor volume |
m3 |
2766 |
2758 |
860 |
1520 |
1760 |
|
HRT |
d |
9,9 |
10,6 |
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